Outline - University of Utahrepository.icse.utah.edu/dspace/bitstream/123456789/10899/1/Oil S… ·...
Transcript of Outline - University of Utahrepository.icse.utah.edu/dspace/bitstream/123456789/10899/1/Oil S… ·...
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Outline
Objective
Process definition
Reaction and kinetic model
Modeling of in-situ combustion
Modeling of in-situ pyrolysis
Modeling of modified in-situ process
Summary
Future work
Acknowledgement
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Objectives
Use preliminary reaction and kinetic models to develop in-situ oil
recovery process analysis in oil shale reservoirs.
STARS – developed by Computer Modeling Group, Inc.
The reaction and kinetic models allow future modifications to improve
accuracy.
Examine the impact of selected process parameters on production
performance
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Process definitions In-situ combustion:
Heat required for kerogen pyrolysis is completely supplied by
combustion reactions inside the reservoir.
Air is pumped into the reservoir and reacts with fuels originally existing
in the reservoir such as kerogen, coke and oil.
In-situ pyrolysis:
Heat is provided by external heating source, such as electrical heating,
EM wave, chemical reactions.
Modified in-situ process:
The recovery process combines in-situ pyrolysis and in-situ pyrolysis,
the purpose is to minimize the energy requirement and maximize the
oil consumption as fuel.
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Process snapshot – 1D O2 mol. fr Temperature So coke conc. kerogen conc.
Producer
Producer
in-situ combustion
in-situ pyrolysis
Injector
Heater Heater
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Reaction models - Hypothesis
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Kinetic models - Hypothesis (Assume 1st for each reacting component)
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Modeling of in-situ combustion
Parameters (base-case): Initial kerogen concentration.
(0.08 lbmol / cf [P.V.]
~ 11.1 wt.%)
Air flow rate.
(100,000 scf / day)
Horizontal permeability.
(1,000 mD)
Vertical permeability.
(10 mD)
Perforation
88 ft
88 ft 88 ft
Porosity : 35 % (vf + vk) (3 ~ 10 % vf)
Residual water : 10 %
Initial pressure : 200 psi
P production : 100 psi
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in-situ combustion Effect of initial kerogen concentration [ 9.7 11.1 12.5 wt.% ]
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in-situ combustion Effect of air flow rate [ 90000 100000 110000 scf / day ]
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in-situ combustion Effect of horizontal permeability [ 500 1000 1500 mD ]
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in-situ combustion Effect of vertical permeability [ 1 10 100 mD ]
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in-situ combustion Effect of vertical permeability on kerogen conversion
Low V. Perm
High V. Perm
bottom middle top
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Modeling of in-situ pyrolysis
Parameters (base-case): Initial kerogen concentration.
(0.08 lbmol / cf [P.V.]
~ 11.1 wt.%)
Heating rate.
(350000 btu / day)
Horizontal permeability.
(10 mD)
Vertical permeability.
(1 mD)
Perforation Heater
88 ft
88 ft
88 ft
x – y plane
x – z plane
Producer
Porosity : 35 % (vf + vk) (3 ~ 10 % vf)
Residual water : 10 %
Initial pressure : 200 psi
P production : 100 psi
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in-situ pyrolysis Effect of initial kerogen concentration [ 9.7 11.1 12.5 wt.% ]
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in-situ pyrolysis Effect of heating source [ 330000 350000 370000 btu / day ]
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in-situ pyrolysis Effect of horizontal permeability [ 1 10 100 mD ]
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in-situ pyrolysis Effect of vertical permeability [ 0.1 1 10 mD ]
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Concept of Modified Process O2 mol. fr Temperature So coke conc. kerogen conc.
Heater in-situ pyrolysis stage
coke + oil
Injector in-situ combustion stage
(coke + oil)1
Completed combustion zone
(coke + oil)2
So2 > So1
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Modeling of Modified Process
Parameters (base-case):
In-situ pyrolysis & combustion
Timing for switch
Air flow rate
Location of producer
Porosity : 35 % (vf + vk) (3 ~ 10 % vf)
Residual water : 10 %
Initial pressure : 200 psi
P production : 100 psi
Perforation Heater
88 ft
88 ft
88 ft
x – y plane
x – z plane
C - Producer
E - Producer
Injector
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Process modification Time to switch [ N/A 900 1200 1500 thday ]
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Process modification Air flow rate [ 50000 70000 90000 sft / day ]
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Process modification Well locations [ 1 – producer (C) 1 – producer (C→E) 2 – producer (E) ]
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Summary Preliminary reaction stoichiometric and kinetic models
A number of assumptions regarding process parameters
Permeability creation for in-situ combustion
Higher kerogen content leads to higher recovery as expected
Influence on in-situ pyrolysis greater than in-situ combustion
In in-situ combustion, higher air flow rate leads to higher recoveries
Permeabilities play important role in both recovery processes
In-situ combustion is energy sufficient – if the process is
operationally viable
Process optimization possible by combining concept of two
processes
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Future work Reaction model
Component characterization, lumping, stoichiometry and kinetics
Significant experimental and modeling issues
Process parameters
Reservoir characterization
Fractures, faults
Reservoir heterogeneity
Geomechanical coupling
Reservoir remedy method
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Acknowledgement Department of Energy
Petroleum Research Center at University of Utah
Utah Heavy Oil Center at University of Utah
Computer Modelling Group LTD.